JPWO2011052290A1 - Polyethylene terephthalate composition, method for producing the same, and polyethylene terephthalate film - Google Patents

Abstract

The polyethylene terephthalate composition of the present invention is a polyethylene terephthalate composition containing 0.01 mol% or more and 1.00 mol% or more of a trifunctional or higher copolymer component with respect to an ethylene terephthalate unit, and the ratio of the weight average molecular weight to the number average molecular weight. (Mw / Mn) is 5.0 or more and 8.0 or less, containing an alkali metal compound as an alkali metal element in an amount of 1.0 mol / ton or more and 3.0 mol / ton or less, and containing a phosphorus compound as a phosphorus element in an amount of 1.5 mol / ton or more and 5.0 mol / ton or less. , O-chlorophenol insoluble matter is less than 0.50 wt%. The present invention provides a polyethylene terephthalate composition excellent in hydrolysis resistance and elongation retention and suitable for a film for solar cells.

Description

The present invention relates to a polyethylene terephthalate composition suitable for solar cell applications having excellent hydrolysis resistance and elongation retention, a production method thereof, and a polyethylene terephthalate film comprising the composition.

Polyethylene terephthalate is excellent in mechanical properties, thermal properties, chemical resistance, electrical properties, and moldability, and is used in various applications.

However, since the mechanical properties of polyethylene terephthalate decrease due to hydrolysis, various studies have been made to suppress hydrolysis when used over a long period of time or when used in a damp state. In particular, a solar cell film requires a service life of 20 years or more outdoors, and therefore requires high hydrolysis resistance and elongation retention.

For example, Patent Document 1 describes a technique of reducing the amount of COOH end groups and improving hydrolysis resistance by compounding a trifunctional or higher functional crosslinking component and a terminal blocking agent with a twin screw extruder.

Patent Document 2 describes a method for producing a polyester containing an inorganic phosphate, and in the examples, phosphoric acid is used in combination.

Patent Document 3 describes polyethylene terephthalate containing buffered phosphorus, and is used in combination with a phosphorus compound in the examples.
JP 2008-31439 A JP 2007-277548 A JP 2008-7750 A

However, the technique of Patent Document 1 is excellent in initial hydrolysis resistance, but since no phosphorus compound is used, the hydrolysis reaction proceeds at an accelerated rate, and long-term hydrolysis resistance is satisfied. Have difficulty. Furthermore, since the crosslinking component is compounded, it reacts non-uniformly and easily generates fine gel-like foreign matters, which is not suitable for film use.
Moreover, since the technique of patent document 2 is inadequate in the ratio and application amount of phosphoric acid and inorganic phosphate, the inorganic phosphate is easily converted into a foreign substance, and has excellent short-term hydrolysis resistance. The long-term hydrolysis resistance required for solar cell applications and the like was insufficient, and the mechanical properties of the film were deteriorated by foreign substances.
Since the technology of Patent Document 3 is insufficient in optimizing the type, ratio, application amount, etc. of the phosphorus compound, the hydrolysis resistance and mechanical properties are insufficient for solar cell applications.
An object of the present invention is to provide a polyethylene terephthalate composition which is excellent in hydrolysis resistance and elongation retention and is suitable for solar cell film use, and a polyethylene terephthalate film comprising the composition, which eliminates these conventional drawbacks. There is.

That is, the object of the present invention is a polyethylene terephthalate composition containing 0.01 mol% or more and 1.00 mol% or less of a trifunctional or higher copolymer component with respect to an ethylene terephthalate unit, and the ratio of the weight average molecular weight to the number average molecular weight ( Mw / Mn) is 5.0 or more and 8.0 or less, containing an alkali metal compound as an alkali metal element at 1.0 mol / ton or more and 3.0 mol / ton or less, a phosphorus compound as a phosphorus element containing 1.5 mol / ton or more and 5.0 mol / ton or less, This is achieved by a polyethylene terephthalate composition having an o-chlorophenol (hereinafter OCP) insoluble content of less than 0.50 wt%.
The object of the present invention is to adjust the pH to 2.0 or more and 6.0 or less when producing a polyethylene terephthalate composition through an esterification reaction or a transesterification reaction using a terephthalic acid component, ethylene glycol, or a tri- or higher functional copolymer component. Production of polyethylene terephthalate composition in which ethylene glycol solution or slurry of prepared phosphoric acid and alkali metal phosphate is added until the end of esterification or transesterification reaction and the start of polycondensation reaction Achieved by the method.
The object of the present invention is also achieved by a polyethylene terephthalate film containing at least one polyethylene terephthalate film layer comprising the above polyethylene terephthalate composition.
Another object of the present invention is a method for producing the above polyethylene terephthalate film, which comprises biaxially stretching an unstretched film and then heat-treating it in a temperature range satisfying the following formula (1). Achieved.
35 ° C ≦ Tm−Th ≦ 90 ° C (1)
Here, Tm: melting point of polyethylene terephthalate composition (° C.), Th: heat treatment temperature (° C.)
The object of the present invention is also achieved by a solar battery backsheet comprising the above polyethylene terephthalate film.

The polyethylene terephthalate composition of the present invention preferably has a COOH end group content of 15 equivalent / ton or less and a cyclic trimer content of 0.50 wt% or less.
The polyethylene terephthalate composition of the present invention preferably has a COOH end group increase (ΔCOOH) of 40 equivalents / ton or less when treated at 155 ° C. for 4 hours under steam.

In the polyethylene terephthalate composition of the present invention, the molar ratio of the alkaline earth metal element and phosphorus element is preferably 0.5 or more and 1.5 or less.
In the polyethylene terephthalate composition of the present invention, the phosphorus compound is preferably phosphoric acid and an alkali metal phosphate.

The production method of the polyethylene terephthalate composition of the present invention is 0.3 times the total acid component when producing a polyethylene terephthalate composition through an esterification reaction using terephthalic acid, ethylene glycol, and a tri- or higher functional copolymer component. It is preferable to add ethylene glycol in an amount of from 0.5 mole to 0.5 moles until the esterification reaction is substantially completed and the polycondensation reaction is started.

The polyethylene terephthalate film of the present invention preferably contains at least one polyethylene terephthalate film layer made of the polyethylene terephthalate composition.

In the polyethylene terephthalate film of the present invention, the plane orientation coefficient of the polyethylene terephthalate film layer is preferably 0.150 or more.
In the polyethylene terephthalate film of the present invention, the amount of COOH end groups in the polyethylene terephthalate film layer is preferably 20 equivalent / ton or less.

The polyethylene terephthalate film of the present invention preferably has an intrinsic viscosity (IV) of the polyethylene terephthalate film layer of 0.65 or more.
The polyethylene terephthalate film of the present invention preferably has an elongation retention of 70% or more after treatment at 125 ° C., 100% RH and 72 hours.

According to the present invention, a polyethylene terephthalate composition having excellent long-term hydrolysis resistance can be provided. Moreover, by using the composition of the present invention as a biaxially stretched film, in addition to applications for magnetic materials, electrical materials such as capacitors, packaging applications, etc., in particular, long-term hydrolysis resistance and elongation retention are required. Can be provided for use in solar cell films.

FIG. 1 is a schematic sectional view showing an example of the configuration of a solar cell using a polyethylene terephthalate film made of the polyethylene terephthalate composition of the present invention.

The polyethylene terephthalate composition of the present invention is a polyethylene terephthalate composition containing 0.01 mol% or more and 1.00 mol% or more of a trifunctional or higher copolymer component with respect to an ethylene terephthalate unit, and the ratio of the weight average molecular weight to the number average molecular weight. (Mw / Mn) is 5.0 or more and 8.0 or less, containing an alkali metal compound as an alkali metal element in an amount of 1.0 mol / ton or more and 3.0 mol / ton or less, and containing a phosphorus compound as a phosphorus element in an amount of 1.5 mol / ton or more and 5.0 mol / ton or less. , A polyethylene terephthalate composition containing less than 0.50 wt% of OCP insoluble matter.

The OCP insoluble matter of the present invention is a residue after 1.0 g of a polyethylene terephthalate composition is dissolved in OCP 50 ml at 160 ° C. for 40 minutes and filtered through a glass filter (3G3).

The polyethylene terephthalate composition of the present invention preferably has 95 mol% or more of ethylene terephthalate unit as a structural unit from the viewpoint of excellent mechanical properties, and 99 mol% or more of ethylene terephthalate unit is preferably hydrolysis resistant. Is more preferable from the viewpoint of improving the quality.

The polyethylene terephthalate composition of the present invention contains a tri- or higher functional copolymer component in an amount of 0.01 mol% or more and 1.00 mol% or less based on the ethylene terephthalate unit, and has excellent hydrolysis resistance and elongation retention, It is necessary from the viewpoint of suppressing the generation of OCP insoluble matter, and 0.05 mol% or more and 0.80 mol% or less is preferable from the viewpoint of excellent hydrolysis resistance and suppressing the generation of OCP insoluble matter. Further, from the viewpoint of improving the stretchability of the film, and particularly capable of further increasing the elongation retention of the film in long-term use by high-stretch stretching and high orientation, 0.07 mol% of a tri- or higher functional copolymer component is added. It is more preferably 0.50 mol% or less, and even more preferably 0.05 mol% or more and 0.20 mol% or less. Any preferred lower limit can be combined with any preferred upper limit. If the copolymerization component having a functionality of 3 or more is less than 0.01 mol%, sufficient hydrolysis resistance and elongation retention cannot be obtained, and if it exceeds 1.00 mol%, OCP insoluble matter is generated. This causes uneven thickness.

The tri- or higher functional copolymerization component includes trimellitic acid, cyclohexanetricarboxylic acid, biphenyltetracarboxylic acid, pyromellitic acid, butanetetracarboxylic acid, trimer acid such as trimer acid obtained by trimerization of long-chain aliphatic carboxylic acid. Carboxylic acid and its anhydrides and esters, glycerin, pentaerythritol, dipentaerythritol, trimethylolpropane, ditrimethylolpropane, trihydroxybenzene, trihydroxyhexane and other polyhydric alcohols, citric acid, dihydroxybenzene carboxylic acid, dihydroxynaphthalenecarboxylic acid Examples thereof include polyvalent hydroxycarboxylic acids such as acids and anhydrides and esters thereof. In particular, the number of functional groups of the copolymer component is preferably 3 from the viewpoint of excellent elongation retention and stretchability, and reducing OCP insoluble matter. As a method for adding such a tri- or higher functional copolymer component, in the case of a polycarboxylic acid ester and a polyhydric alcohol component, it is added before the transesterification reaction, and in the case of a polyvalent carboxylic acid, it is added as an ethylene glycol solution or slurry. It is preferable from the viewpoint of improving the handleability and reducing the OCP insoluble matter.

The molecular weight distribution of the polyethylene terephthalate composition of the present invention is such that the ratio of the weight average molecular weight to the number average molecular weight (Mw / Mn) is 5.0 or more and 8.0 or less. It is necessary from the viewpoint of reduction. Further, Mw / Mn is preferably set to 5.0 or more and 7.0 or less from the viewpoint of reducing OCP insoluble matter. When Mw / Mn is less than 5.0, sufficient elongation retention cannot be obtained. On the other hand, if Mw / Mn exceeds 8.0, OCP insoluble matter is easily generated and the melt viscosity becomes high, so that the castability during film formation is lowered.

Mw / Mn of 5.0 or more and 8.0 or less can be achieved by setting the intrinsic viscosity to 0.70 or more in the presence of a tri- or higher functional copolymer component. In order to increase Mw / Mn, it is effective to increase the degree of polymerization by solid phase polymerization. In addition, Mw / Mn also depends on the copolymer component, and in order to obtain a higher Mw / Mn, it is necessary to increase the copolymer component having three or more functional groups or use a copolymer component having a larger number of functional groups. It is valid.
Here, regarding the molecular weight of the polyethylene terephthalate composition of the present invention, the number average molecular weight is preferably 10,000 or more from the viewpoint of excellent hydrolysis resistance and elongation retention.

The polyethylene terephthalate composition of the present invention needs to contain an alkali metal compound in an amount of 1.0 mol / ton or more and 3.0 mol / ton or less as an alkali metal element from the viewpoint of excellent hydrolysis resistance. The content is preferably from / ton to 2.0 mol / ton from the viewpoint of excellent hydrolysis resistance. If the content of the alkali metal compound is less than 1.0 mol / ton as an alkali metal element, sufficient hydrolysis resistance cannot be obtained. On the other hand, if it exceeds 3.0 mol / ton as an alkali metal element, the hydrolysis reaction is promoted.

Examples of the alkali metal element contained in the polyethylene terephthalate composition of the present invention include sodium, potassium, and lithium. Of these, sodium or potassium is preferable from the viewpoint of excellent hydrolysis resistance. The compound containing an alkali metal element is preferably a hydroxide or a phosphate from the viewpoint of excellent hydrolysis resistance. The compound containing an alkali metal element is more preferably a sodium phosphate salt from the viewpoint of solubility in polyester. Of the sodium phosphate salt, sodium dihydrogen phosphate is more preferable from the viewpoint of excellent hydrolysis resistance.

From the viewpoint of excellent hydrolysis resistance, the polyethylene terephthalate composition of the present invention must contain a phosphorus compound as a phosphorus element in a range of 1.5 mol / ton to 5.0 mol / ton, and a phosphorus element as 2.0 mol It is preferably contained in the range of / ton to 4.0 mol / ton. If the phosphorus compound content is less than 1.5 mol / ton as a phosphorus element, sufficient hydrolysis resistance cannot be obtained. On the other hand, if the phosphorus element content exceeds 5.0 mol / ton, the COOH end group tends to increase due to the polycondensation reaction delay, and the hydrolysis reaction is promoted. As the compound containing phosphorus element, phosphoric acid, phosphate ester, alkali metal phosphate, and the like can be used. From the standpoint of excellent hydrolysis resistance, it is preferable to use phosphoric acid and an alkali metal phosphate in combination.

Since the OCP insoluble matter in the polyethylene terephthalate composition becomes a foreign substance when formed into a film, the content thereof needs to be less than 0.50 wt% with respect to the polyethylene terephthalate composition. When the OCP insoluble matter is 0.50 wt% or more, it becomes a defect such as fish eye when it is made into a film.

In order to make the OCP insoluble matter less than 0.50 wt%, it is effective to shorten the polycondensation reaction time for reaction in the molten state. For example, the intrinsic viscosity in the melt polymerization may be finished at 0.50 or more and 0.60 or less, and solid phase polymerization may be performed in the range of 210 ° C to 230 ° C. Solid-phase polymerization has a lower reaction temperature and lower molecular mobility than ordinary polycondensation reactions, so that gelation due to crosslinking is difficult to proceed and is effective in reducing OCP insoluble matter.

The polyethylene terephthalate composition of the present invention preferably has a COOH end group amount of 15 equivalents / ton or less, more preferably 12 equivalents / ton, from the viewpoint of excellent hydrolysis resistance.

The cyclic trimer contained in the polyethylene terephthalate composition of the present invention is preferably 0.50 wt% or less from the viewpoint of excellent hydrolysis resistance. The cyclic trimer is a trimer of an ethylene terephthalate unit trimmed by an intramolecular reaction. In the melted state of the polyethylene terephthalate composition, the cyclic trimer content is about 1.0 wt%. It is known to be saturated. This cyclic trimer can be reduced in content by removing it in the solid phase when the polyethylene terephthalate composition is solid-phase polymerized, but it is produced again when the polyethylene terephthalate composition is melted. Is about 1.0 wt% corresponding to the saturation concentration. Such a cyclic trimer is produced by esterifying OH end groups and COOH end groups in the molecule in the molten state of the polyethylene terephthalate composition. It has the effect of suppressing the increase in COOH end groups when the terephthalate composition is melted.
In order to make this cyclic trimer 0.50 wt% or less, the temperature condition during solid phase polymerization may be 210 ° C. or higher and 230 ° C. or lower.

The polyethylene terephthalate composition of the present invention has 40 equivalents of COOH end group increase (hereinafter referred to as ΔCOOH) when an unstretched film is treated under steam at 155 ° C. for 4 hours from the viewpoint of excellent elongation retention. / ton or less, more preferably 30 equivalent / ton or less.
To reduce ΔCOOH to 40 equivalents / ton or less, it is effective to reduce the COOH end groups before treatment as much as possible, but there is a limit to reducing the COOH end groups without using end-capping agents. Suppressing the decomposition reaction rate with a buffering agent such as phosphoric acid / alkali metal phosphate is effective from the viewpoint of excellent hydrolysis resistance.

The molar ratio of the alkaline earth metal element and phosphorus element contained in the polyethylene terephthalate composition of the present invention is from 0.5 to 1.5 in terms of hydrolysis resistance and excellent electrostatic application characteristics during film formation. It is preferable that the molar ratio is 0.7 or more and 1.3 or less. Any preferred lower limit can be combined with any preferred upper limit. The alkaline earth metal compound is preferably an acetate salt from the viewpoint of excellent polycondensation reactivity and solubility in polyethylene terephthalate, and suppresses OCP insolubles. Specifically, magnesium acetate or calcium acetate. Can be mentioned.

The polyethylene terephthalate composition of the present invention can be produced by performing a polycondensation reaction and, if necessary, solid phase polymerization through an esterification reaction or a transesterification reaction.

As a manufacturing method of such a polyethylene terephthalate composition, after performing esterification reaction or transesterification, it can manufacture by performing a polycondensation reaction.
When performing a polycondensation reaction via an ester exchange reaction, a known catalyst such as magnesium acetate, calcium acetate, zinc acetate, manganese acetate, cobalt acetate, tetrabutoxy titanate, aluminum acetate, or lithium acetate is used as the ester exchange reaction catalyst. be able to. Of these, magnesium acetate and calcium acetate are preferably used as catalysts from the viewpoint of excellent hydrolysis resistance and electrostatic application characteristics during film formation.

In the method for producing a polyethylene terephthalate composition of the present invention, as a method for adding a tri- or higher functional copolymer component, it is possible to change the addition time depending on the type of terminal group of the copolymer component, transesterification reactivity, polycondensation reactivity From the viewpoint of improving handling properties, it is preferable. Specifically, when the terminal group of the copolymer component is an OH group, it is preferable to add the copolymer component at any time from the transesterification reaction to the start of the polycondensation reaction. Is a COOH group, the copolymerization component is preferably added after the transesterification reaction, and when the terminal group of the copolymerization component is an ester group, it is preferably added before the transesterification reaction. In addition, in the case of a compound having both OH group and COOH group, such as hydroxycarboxylic acid, the addition method in the case of COOH group, that is, adding a copolymer component after the transesterification reaction is transesterification, polycondensation This is preferable from the viewpoint of improving the reactivity.

As the polycondensation reaction catalyst used in the polycondensation reaction, known compounds can be used. For example, antimony trioxide, titanium alkoxide, titanium chelate compound, germanium dioxide and the like can be preferably exemplified. Of these, antimony trioxide is more preferable from the viewpoint of improving the polycondensation reactivity and heat resistance.

In the method for producing a polyethylene terephthalate composition of the present invention, from the viewpoint of reducing ΔCOOH, the pH is 2.0 or more and 6.0 or less until the esterification reaction or transesterification reaction is substantially completed and the polycondensation reaction is started. It is added as an ethylene glycol solution or slurry of phosphoric acid and alkali metal phosphate prepared in the above. Further, from the viewpoint of excellent elongation retention, the pH of the ethylene glycol solution or slurry is preferably 2.0 or more and 5.0 or less.

As the polycondensation reaction conditions, it is preferable that the final temperature is 275 ° C. or more and 285 ° C. or less from the viewpoint of reducing COOH end groups. Further, it is preferable to form chips when the intrinsic viscosity of the polyethylene terephthalate composition reaches 0.50 or more and 0.60 or less from the viewpoint of reducing COOH end groups and reducing OCP insoluble matter. In addition, reducing the amount of polyethylene terephthalate raw material charged in the polymerization vessel to shorten the polycondensation reaction time is also effective in reducing COOH end groups, but in this case, the production amount per batch is reduced.

The polyethylene terephthalate composition thus obtained can improve the elongation retention by performing solid phase polymerization and further reducing the COOH end groups.
In the method for producing a polyethylene terephthalate composition of the present invention, a polycondensation reaction is carried out through an esterification reaction to obtain a polyethylene terephthalate composition. Addition before the start of the condensation reaction is preferred from the viewpoint of improving polycondensation reactivity. In particular, in the case of an esterification reaction, since many unreacted COOH end groups remain, after the esterification reaction is substantially completed and before the polycondensation reaction is started, a trifunctional or higher functional copolymer component is added. By adding as an ethylene glycol solution or slurry, COOH end groups can be esterified with ethylene glycol, and the amount of COOH end groups can be reduced. As the amount of ethylene glycol at this time, the total amount of ethylene glycol added between the end of the esterification reaction and the start of the polycondensation reaction is 0.3 mol times or more based on the total acid components contained in the polyethylene terephthalate composition. 0.5 mol times or less is preferable from the viewpoint of reducing the amount of COOH end groups and reducing OCP insoluble matter. As the total amount of ethylene glycol added between the end of the esterification reaction and the start of the polycondensation reaction, polyethylene terephthalate If it is within the range of 0.3 mol times or more and 0.5 mol times or less with respect to all the acid components contained in the composition, only ethylene glycol may be added separately.

Hereinafter, an example of a specific production method of the polyethylene terephthalate composition of the present invention will be described in the case of using trimethyl trimellitic acid (trifunctional) as a tri- or higher functional copolymer component, but is not limited thereto. Other polyfunctional compounds can also be produced by the same method.

Charge dimethyl terephthalate, trimethyl trimellitic acid, and ethylene glycol as monomers. Trimethyl trimellitic acid at this time is, for example, 0.01 mol% or more and 1.00 mol% with respect to dimethyl terephthalate in order to make the elongation retention after treatment for 72 hours at a temperature of 125 ° C, 100% RH, 70% or more. The following. Increasing the elongation retention rate during wet heat treatment is important when used for a long period of time in an environment with a large humidity change, such as for solar cell applications. As a transesterification reaction catalyst, magnesium acetate tetrahydrate and antimony trioxide are used. After melting in a nitrogen atmosphere at 150 ° C., the temperature is raised to 230 ° C. with stirring, and a transesterification reaction is performed while distilling methanol. In this case, it is sufficient that the magnesium acetate tetrahydrate is 0.04 parts by weight or more and 0.08 parts by weight or less with respect to 100 parts by weight of the polyethylene terephthalate composition from the viewpoint of transesterification reactivity and electrostatic application characteristics. The addition amount of antimony trioxide is sufficient if it is 0.025 parts by weight or more and 0.035 parts by weight or less with respect to the polyethylene terephthalate composition from the viewpoint of polycondensation reactivity.

After completion of the transesterification reaction, 0.019 parts by weight of phosphoric acid (corresponding to 1.9 mol / ton of phosphorus atom) and 0.027 parts by weight of sodium dihydrogen phosphate dihydrate (1.7 atoms of phosphorus atom) per 100 parts by weight of the polyethylene terephthalate composition. mol / ton, equivalent to 1.7 mol / ton of sodium atom) is added an ethylene glycol solution (pH 5.0) in 0.5 parts by weight of ethylene glycol. At this time, the phosphorus atomic weight is 1.5 mol / ton or more and 5.0 mol / ton or less with respect to the polyethylene terephthalate composition in order to make the elongation retention after treatment for 125 hours at a temperature of 125 ° C. and a humidity of 100% 70% or more. The sodium metal atomic weight is 1.0 mol / ton or more and 3.0 mol / ton or less. Furthermore, it is preferable to adjust the molar ratio of sodium atom / phosphorus atom to 0.5 or more and 1.5 or less, and adjust the ethylene glycol solution of phosphoric acid and sodium dihydrogen phosphate dihydrate to pH 2.0 or more and 6.0 or less. Can be 40 equivalents / ton or less, and the elongation retention can be 80% or more.

In the polycondensation reaction, for example, the final reached temperature is 280 ° C. and the degree of vacuum is 0.1 Torr. At this time, by setting the melt viscosity at the time of discharge to an intrinsic viscosity of 0.50 or more and 0.60 or less, it is possible to achieve OCP insoluble matter less than 0.50 wt%.

The obtained polymer chip is dried and crystallized, for example, at 150 ° C. for 4 hours at a vacuum degree of 0.1 Torr, and then subjected to solid phase polymerization at 220 ° C. and a vacuum degree of 0.3 Torr for 6 hours, thereby producing the polyethylene terephthalate composition of the present invention. Get. As drying and crystallization conditions at this time, it is sufficient to dry under reduced pressure at 140 to 160 ° C. for 4 hours or more. The solid phase polymerization conditions are 210 ° C. or higher and 230 ° C. or lower, and a vacuum degree of 0.3 Torr or lower and solid phase polymerization for 4 hours or longer and 10 hours or shorter, resulting in Mw / Mn 5.0 or higher and 8.0 or lower, COOH end group 15 equivalent / ton or lower. The cyclic trimer can be 0.50 wt% or less.

The polyethylene terephthalate composition thus obtained can be dried by a conventional method, and then extruded with a normal extruder and a T die to obtain an unstretched film, which can be converted into a film through a biaxial stretching process. The specific method will be described next.
As a manufacturing method, first, raw materials are charged into an extruder (or multiple extruders when laminating multiple layers by the coextrusion method), melted and extruded from the die (coextrusion in the case of a laminated structure). Then, it is closely cooled and solidified by static electricity on a cooled drum cooled to a surface temperature of 10 ° C. or more and 60 ° C. or less to produce an unstretched film.

The obtained unstretched film is biaxially stretched at a temperature not lower than the glass transition temperature Tg of the unstretched film. As the biaxial stretching method, in addition to the sequential biaxial stretching method in which the stretching in the longitudinal direction and the width direction is separated as described above, the simultaneous biaxial stretching method in which the stretching in the longitudinal direction and the width direction is performed simultaneously. both are fine.
The polyethylene terephthalate film of the present invention contains at least one polyethylene terephthalate film layer (hereinafter referred to as P layer) made of the above polyethylene terephthalate composition, and may be a single layer, but a different material on the P layer. It is also preferable to laminate another layer consisting of
As a method for forming another layer made of a different material on the P layer, in addition to the above-described coextrusion method, melt lamination method, solution lamination method, thermal lamination method, etc., dry methods such as vapor deposition method, sputtering method, etc. A wet method such as a plating method or a plating method is also preferable. Examples of a method for forming another layer made of a different material by a coating method include an in-line coating method applied during film formation and an off-line coating method applied after film formation, both of which can be used. The in-line coating method is more preferable because it is efficient at the same time as film formation and has high adhesion to a film substrate. Prior to coating, it is also preferable to pre-corona-treat the film surface.
The film having the P layer made of the polyethylene terephthalate composition obtained by the above-mentioned method not only has excellent hydrolysis resistance, but also has a crosslinked structure in the film, so the movement of molecular chains is restricted and water enters. It is possible to suppress the higher-order structure change after hydrolysis, and it is possible to obtain drastically higher moisture and heat resistance than conventional polyethylene terephthalate films. Specifically, for example, it is suitable for a long-term use in an environment with a large humidity change such as a solar cell application, and further, a temperature retention of 125 ° C., a humidity of 100% RH, and an elongation retention rate after 72 hours of treatment of 80% or more. It is suitable for an application that is used for a longer period of time. The elongation retention after treatment for 96 hours at a temperature of 125 ° C. and humidity of 100% RH is more preferably 10% or more, and even more preferably 20% or more.
In order to further increase the elongation retention rate after processing for 72 hours at a temperature of 125 ° C. and a humidity of 100% RH, the chip is supplied to the extruder in a nitrogen atmosphere, and the time until extrusion from the T die is shortened. It is effective to reduce the COOH end group and to make the film stretch ratio 10 times or more, particularly 12 times or more in terms of effective surface magnification. In order to set the elongation retention after treatment for 96 hours at a temperature of 125 ° C. and a humidity of 100% to 10% or more, it is effective to set the effective surface magnification to 13 times or more and the plane orientation coefficient to 0.150 or more.
In the polyethylene terephthalate film of the present invention, from the viewpoint of excellent hydrolysis resistance, the COOH end group amount after film formation of the polyethylene terephthalate composition constituting the P layer is preferably 20 equivalent / ton or less, more preferably Is 18 equivalent / ton or less, more preferably 16 equivalent / ton or less. If the amount of COOH end groups after film formation of the polyethylene terephthalate composition constituting the P layer is 20 equivalents / ton or less, the catalytic action of protons on the COOH end groups is suppressed, and the progress of deterioration is prevented by preventing hydrolysis. Can be prevented. In order to reduce the number of COOH end groups to 20 equivalents / ton or less, [1] lowering the COOH of the polyethylene terephthalate composition before melt extrusion (solid phase polymerization, use of end-capping agents, etc.), [2] additives (3) Suppression of decomposition reaction (buffering agent, antioxidant, heat stabilizer, etc.), [3] Nitrogen blowing at the time of melt extrusion, and a method of blocking oxygen in the extruder may be combined. In addition, a method of adding a buffering agent or a terminal blocking agent at the time of molding is also effective.

Here, in the polyethylene terephthalate film of the present invention, the plane orientation coefficient of the P layer is preferably 0.150 or more from the viewpoint of excellent hydrolysis resistance and elongation retention. The plane orientation coefficient of the P layer is more preferably 0.155 or more, further preferably 0.160 or more, and particularly preferably 0.168 or more. When the plane orientation coefficient is 0.150 or more, oriented crystallization is sufficient, there are many oriented crystallized parts, and the mobility of the amorphous part can be suppressed, thereby preventing water from entering between the molecular chains. High moisture and heat resistance can be obtained.
Here, in the polyethylene terephthalate film of the present invention, since the polyethylene terephthalate composition forming the P layer has a branched structure, it is less regular than a linear polyethylene terephthalate having no branched structure, and is in a molten state. Since the molecular chains are strongly entangled in a non-oriented state after being rapidly cooled, it is difficult to align them compared to linear polyethylene terephthalate having no branched structure. In order to make the plane orientation coefficient 0.150 or more, [1] In the case of simultaneous biaxial stretching, the stretching temperature is in the range of the glass transition temperature Tg of the polyethylene terephthalate composition to Tg + 15 ° C or less, and [2] sequential biaxial stretching. In this case, the first axis stretching is set to a temperature of the glass transition temperature Tg or more of the polyethylene terephthalate composition to Tg + 15 ° C. or less (more preferably Tg + 10 ° C. or less), and the second axis stretching is Tg + 5 ° C. or more to Tg + 25 ° C. As the temperature in the following range, the area stretching ratio may be 12 times or more, more preferably 13 times or more, further preferably 14 times or more, particularly preferably 15 times or more, and most preferably 16 times or more. .

  In order to complete the crystal orientation of the obtained polyethylene terephthalate film and to impart flatness and dimensional stability, a heat treatment is performed for 1 second to 30 seconds at a temperature lower than the melting point of the polyethylene terephthalate composition and lower than the melting point, Slowly cool to room temperature after uniform cooling. In general, when the heat treatment temperature Th is low, the thermal contraction rate of the film increases, so that the heat treatment temperature Th is preferably higher in order to impart high thermal dimensional stability. However, if the heat treatment temperature Th is too high, the amorphous part is relaxed and the molecular mobility becomes high, so that hydrolysis is likely to occur, and thermal crystallization after hydrolysis is promoted and brittle in a humid heat atmosphere. Progresses. Therefore, in the method for producing a polyethylene terephthalate film of the present invention, the heat treatment temperature Th is such that the difference Tm-Th from the melting point Tm of the polyethylene terephthalate composition is 35 ° C. or more and 90 ° C. or less. This Tm-Th is preferably 50 ° C. or higher and 80 ° C. or lower, more preferably 55 ° C. or higher and 75 ° C. or lower. Any preferred lower limit can be combined with any preferred upper limit. Note that by controlling Th, the minute endothermic peak temperature Tmetap of the P layer can be controlled. Moreover, you may perform a 3-12% relaxation process in the width direction or a longitudinal direction as needed in the said heat processing process. Subsequently, if necessary, the P layer of the polyethylene terephthalate film of the present invention can be formed by performing corona discharge treatment or the like in order to further improve the adhesion to other materials.

  Regarding the P layer in the polyethylene terephthalate film of the present invention, the difference Tm−Tmetap between the melting point Tm of the P layer obtained by differential scanning calorimetry (hereinafter referred to as DSC) and the minute endothermic peak temperature Tmetap of the P layer is 40 ° C. or more and 90 ° C. It is preferable that it becomes below ℃. Here, the T metap and melting point Tm of the P layer are values obtained by DSC in the temperature raising process (temperature raising rate: 20 ° C./min). Specifically, by a method based on JIS K 7121 (1999), heating from 25 ° C. to 300 ° C. at a rate of temperature increase of 20 ° C./min (1stRUN), holding in that state for 5 minutes, and then 25 ° C. or less Tmetap, the minute endothermic peak temperature before the crystal melting peak in the DSC measurement chart of 1stRUN, which was obtained by rapidly cooling to room temperature and raising the temperature from room temperature to 300 ° C at a rate of 20 ° C / min (2ndRUN). , Tm is the peak top temperature in the 2ndRUN crystal melting peak.

  Tm-Tmetap is more preferably 50 ° C or higher and 80 ° C or lower, further preferably 55 ° C or higher and 75 ° C or lower, and particularly preferably 60 ° C or higher and 75 ° C or lower. Any preferred lower limit can be combined with any preferred upper limit. In the polyethylene terephthalate film of the present invention, by reducing the difference Tm-Tmetap between the melting point Tm of the P layer and the minute endothermic peak temperature Tmetap of the P layer to 40 ° C. or more and 90 ° C. or less, both shrinkage reduction and moisture heat resistance can be achieved. .

  Furthermore, in the polyethylene terephthalate film of the present invention, the T metap of the P layer is preferably 160 ° C. or higher and Tm−40 ° C. (however, Tm−40 ° C.> 160 ° C.). Tmetap is more preferably 170 ° C. or more and Tm−50 ° C. (however, Tm−50 ° C.> 170 ° C.), and further preferably Tmetap is 180 ° C. or more and Tm−55 ° C. (however, Tm−55 ° C.> 180.degree. C.) or less, and particularly preferably Tmetap is 180.degree. C. or more and Tm-60.degree. C. (however, Tm-60.degree. C.> 180.degree. C.). Any preferred lower limit can be combined with any preferred upper limit. When Tmetap is set to 160 ° C. or higher, the thermal contraction of the film is prevented from becoming too large. For example, when the polyester film of the present invention is used as a film for a solar battery back sheet, It is possible to prevent the warpage of the solar cell when it is incorporated into the solar cell and used for a long time.

In the polyethylene terephthalate film of the present invention, the melting point Tm of the P layer is preferably 240 ° C. or higher, more preferably 250 ° C. or higher, from the viewpoint of heat resistance.
The polyethylene terephthalate film of the present invention is preferably used both in the case of a single layer consisting of only the P layer and in the case of a laminated structure with another layer (hereinafter referred to as P ′ layer) made of a different material. In the case of a laminated structure, it is preferable that the ratio of the P layer is 40% or more of the entire polyethylene terephthalate film in order to exhibit the high moisture and heat resistance effect of the polyester layer. More preferably, it is 50% or more, more preferably 70% or more, and particularly preferably 80% or more.
In the polyethylene terephthalate film of the present invention, the thickness of the P layer is preferably 10 μm or more and 500 μm or less, more preferably 20 μm or more and 300 μm or less, and further preferably 25 μm or more and 200 μm or less. Any preferred lower limit can be combined with any preferred upper limit. By setting the thickness of the P layer to 10 μm or more and 500 μm or less, the moisture and heat resistance of the film can be made excellent, and the thickness of the entire solar cell does not become too large.
The total thickness of the polyethylene terephthalate film of the present invention is preferably 10 μm or more and 500 μm or less, more preferably 20 μm or more and 300 μm or less, and further preferably 25 μm or more and 200 μm or less. Any preferred lower limit can be combined with any preferred upper limit. By setting the thickness to 10 μm or more and 500 μm or less, it is easy to ensure the flatness of the film, and the thickness of the entire solar cell does not become too large.

  Examples of the P ′ layer laminated on the P layer in the polyethylene terephthalate film of the present invention include a polyester layer for imparting a function, an antistatic layer, an adhesion layer with other materials, and an ultraviolet resistant layer for having ultraviolet resistance. An arbitrary layer can be formed according to the application to be used, such as a flame retardant layer for imparting flame retardancy and a hard coat layer for enhancing impact resistance and scratch resistance. As a specific example, when the polyethylene terephthalate film of the present invention is used as a film for a solar battery back sheet, other sheet materials, easy adhesion for improving adhesion with ethylene vinyl acetate embedded with a power generation element In addition to the layer, the ultraviolet resistant layer, and the flame retardant layer, a conductive layer that improves a voltage at which a partial discharge phenomenon, which is an index of insulation, is generated can be formed.

  In the polyethylene terephthalate film of the present invention, when a layer made of another polyester having ethylene terephthalate as a main repeating unit is formed as the P ′ layer in the P layer, the intrinsic viscosity (IV) of the polyester resin constituting the other polyester Is preferably 0.65 or more. More preferably, it is 0.68 or more, More preferably, it is 0.70 or more, Most preferably, it is 0.72 or more. When the IV of the other polyester resin constituting the P ′ layer is 0.65 or more, the molecular weight is moderate, and the hydrolysis of the P ′ layer and subsequent thermal crystallization proceed excessively when exposed to a humid heat atmosphere. Therefore, the P ′ layer is not easily brittle and the film is not easily broken. Therefore, the function can be imparted without impairing the high moisture and heat resistance obtained by the P layer. The upper limit of IV is not particularly determined, but is preferably 1.0 or less, more preferably 0.90 or less, from the viewpoint of preventing polymerization time from becoming disadvantageous in terms of cost and difficulty in melt extrusion. is there.

  In the polyethylene terephthalate film of the present invention, the number of COOH end groups of other polyesters constituting the P ′ layer is preferably 20 equivalents / ton or less. More preferably, it is 18 equivalent / ton or less, More preferably, it is 16 equivalent / ton or less. If the number of COOH end groups is 20 equivalents / ton or less, the catalytic action of protons in the COOH end groups of the P ′ layer is weak and hydrolysis of the P ′ layer and subsequent thermal crystallization do not proceed excessively. The P ′ layer is not easily embrittled and the film is not easily broken. In addition, the COOH end group proton generated in the P ′ layer is difficult to diffuse into the P layer, and does not promote hydrolysis of the P layer. Therefore, the function can be imparted without impairing the high moisture and heat resistance obtained by the P layer.

In the polyethylene terephthalate film of the present invention, when forming another polyester layer as the P ′ layer, a heat resistant stabilizer, an oxidation resistant stabilizer, an ultraviolet absorber, as long as the effects of the present invention are not impaired as necessary. By blending additives such as UV stabilizers, organic / inorganic easy lubricants, organic / inorganic fine particles, fillers, nucleating agents, dyes, dispersants, coupling agents, etc. Functions can also be added.
The polyethylene terephthalate composition of the present invention produced in this way has a small amount of COOH end groups and good resistance to hydrolysis in a short period of time. A film comprising the polyethylene terephthalate composition of the present invention is a solar Long-term hydrolysis resistance and elongation retention required for applications such as battery films, particularly solar battery back sheets, are also good. In addition, the polyethylene terephthalate composition of the present invention takes advantage of its properties, such as copper-clad laminates, adhesive tapes, flexible printed boards, membrane switches, sheet heating elements, flat cables, and other electrically insulating materials, capacitor materials, and automotive materials. It can be suitably used for applications in which flame retardancy is important, such as building materials.

  The configuration of the solar cell backsheet using the polyethylene terephthalate film of the present invention can be any configuration, and an ethylene-vinyl acetate copolymer (hereinafter referred to as EVA) that seals the power generating element on the polyethylene terephthalate film of the present invention. ) EVA adhesion layer that improves adhesion to the adhesive layer, an anchor layer for raising adhesion with the EVA adhesion layer, a water vapor barrier layer, an ultraviolet absorption layer for preventing ultraviolet degradation, a light reflection layer for enhancing power generation efficiency, The solar cell backsheet of the present invention is formed by forming a light absorption layer for expressing design properties, an adhesive layer for bonding the layers, and the like.

  The EVA adhesion layer is a layer that improves adhesion to the EVA resin that seals the power generation element, and is disposed on the side closest to the power generation element, and contributes to adhesion between the backsheet and the system. The material is not particularly limited as long as adhesion with EVA resin is expressed. For example, EVA, EVA and ethylene-methyl acrylate copolymer (EMA), ethylene-ethyl acrylate copolymer (EEA), ethylene A mixture of butyl acrylate copolymer (EBA), ethylene-methacrylic acid copolymer (EMAA), ionomer resin, polyester resin, urethane resin, acrylic resin, polyethylene resin, polypropylene resin, polyamide resin or the like is preferably used. Moreover, in order to improve the adhesiveness to the back sheet | seat of an EVA contact bonding layer as needed, forming an anchor layer is also performed preferably. The material is not particularly limited as long as adhesion to the EVA adhesion layer is expressed, and for example, a mixture containing a resin as a main constituent such as an acrylic resin or a polyester resin is preferably used.

  The water vapor barrier layer is a layer for preventing water vapor from entering from the back sheet side in order to prevent water vapor deterioration of the power generation element when the solar cell is configured. It is formed by providing an oxide such as silicon oxide or aluminum oxide or a metal layer such as aluminum on the film surface by a known method such as vacuum deposition or sputtering. The thickness is preferably in the range of usually 10 nm or more and 20 nm or less. In this case, both the case where the gas barrier layer is provided directly on the polyester film of the present invention and the case where the gas barrier layer is provided on another film and this film is laminated on the film surface of the present invention are preferably used. Moreover, the method of laminating | stacking metal foil (for example, aluminum foil) on the film surface can also be used. In this case, the thickness of the metal foil is preferably in the range of 10 μm to 50 μm from the viewpoint of workability and gas barrier properties.

  The ultraviolet absorbing layer is a layer for blocking ultraviolet rays in order to prevent ultraviolet degradation of the resin in the inner layer, and any layer can be used as long as it has a function of blocking ultraviolet rays of 380 nm or less. The light reflecting layer is a layer that reflects light, and by forming this layer, the inner layer resin is prevented from UV degradation, or the light that reaches the back sheet without being absorbed by the solar cell system is reflected. This layer is used to increase the power generation efficiency by returning to the system side, and is a layer containing white pigments such as titanium oxide and barium sulfate, or bubbles. The light absorbing layer is a layer that absorbs light, and is a layer that is used to prevent UV degradation of the resin in the inner layer or improve the design of the solar cell by forming this layer.

  The solar cell back sheet of the present invention is formed by combining each of the above layers and the polyethylene terephthalate film of the present invention. In the solar battery backsheet of the present invention, it is not necessary to form all of the above layers as independent layers, and it is also a preferred form to form a function integration layer having a plurality of functions. When the polyethylene terephthalate film of the present invention already has a specific function, the layer having the specific function can be omitted. For example, when the polyethylene terephthalate film of the present invention includes a layer containing a white pigment or air bubbles and has light reflectivity, the light reflective layer is included, and the structure including a layer including a light absorber has light absorption. In such a case, the absorption layer may be omitted, and in the case of a configuration including a layer containing an ultraviolet absorber, the ultraviolet absorption layer may be omitted.

  Since the polyethylene terephthalate film of the present invention is superior in moisture and heat resistance as compared with the conventional polyethylene terephthalate film, the solar cell backsheet including this film has higher moisture and heat resistance than the conventional backsheet. Here, in the solar battery backsheet, in order for the backsheet to exhibit the high moisture and heat resistance effect of the polyethylene terephthalate film of the present invention, the volume ratio of the P layer to the entire backsheet is preferably 10% or more. More preferably, it is 20% or more, more preferably 25% or more, particularly preferably 30% or more, and most preferably 40% or more.

  The solar cell backsheet using the polyethylene terephthalate film of the present invention can be made more durable or thinner than the conventional solar cell by taking advantage of its high heat and humidity resistance than the conventional backsheet. An example of the configuration is shown in FIG. A power generating element connected with a lead wire for taking out electricity (not shown in FIG. 1) is sealed with a transparent filler 2 such as EVA resin, a transparent substrate 4 such as glass, a back sheet 1 and Although it is configured by adhering a so-called resin sheet, it is not limited to this and can be used for any configuration.

  The power generating element 3 converts light energy of sunlight 5 into electric energy, and is based on crystalline silicon, polycrystalline silicon, microcrystalline silicon, amorphous silicon, copper indium selenide, compound semiconductor, dye Arbitrary elements such as a sensitizing system can be used by connecting them in series or in parallel depending on the desired voltage or current depending on the purpose.

  Since the transparent substrate 4 having translucency is located on the outermost surface layer of the solar cell, a transparent material having high weather resistance, high contamination resistance, and high mechanical strength characteristics in addition to high transmittance is used. In the solar cell of the present invention, the transparent substrate 4 having translucency can use any material as long as the above properties are satisfied. Examples thereof include glass, ethylene tetrafluoride-ethylene copolymer (ETFE), Polyvinyl fluoride resin (PVF), polyvinylidene fluoride resin (PVDF), polytetrafluoroethylene resin (TFE), tetrafluoroethylene-hexafluoropropylene copolymer (FEP), polytrifluoroethylene chloride resin ( Fluorine resins such as CTFE) and polyvinylidene fluoride resins, olefin resins, acrylic resins, and mixtures thereof are preferred. In the case of glass, it is more preferable to use a tempered glass. Moreover, when using the resin-made translucent base material, what extended | stretched the said resin uniaxially or biaxially from a viewpoint of making mechanical strength excellent is also used preferably.

  In addition, in order to impart adhesion to the EVA resin that is a sealing material agent for the power generation element, it is preferable to subject the surface to corona treatment, plasma treatment, ozone treatment, and easy adhesion treatment. Is called.

  The filler 2 for sealing the power generation element is formed by covering and fixing the unevenness of the surface of the power generation element with resin, protecting the power generation element from the external environment, and for the purpose of electrical insulation, In order to adhere to the back sheet and the power generation element, a material having high transparency, high weather resistance, high adhesion, and high heat resistance is used. Examples thereof include ethylene-vinyl acetate copolymer (EVA), ethylene-methyl acrylate copolymer (EMA), ethylene-ethyl acrylate copolymer (EEA) resin, ethylene-methacrylic acid copolymer (EMAA), Ionomer resins, polyvinyl butyral resins, and mixtures thereof are preferably used. Of these resins, ethylene-vinyl acetate is more preferably used from the viewpoint of excellent balance of weather resistance, adhesiveness, filling property, heat resistance, cold resistance, and impact resistance.

Here, in the solar cell of the present invention, the above-described solar cell backsheet 1 is installed on the back surface of the layer made of the filler 2 sealing the power generating element.
As described above, by incorporating the solar cell back sheet using the polyethylene terephthalate film of the present invention into a solar cell system, it is possible to obtain a solar cell system that is more durable and / or thinner than conventional solar cells. It becomes. The solar cell of the present invention can be suitably used for various applications without being limited to outdoor use and indoor use such as a solar power generation system and a power source for small electronic components.

(A) 0.1 g of intrinsic viscosity polymer was dissolved in 10 ml of o-chlorophenol at 160 ° C. for 20 minutes and measured at 25 ° C.
(B) Quantitative determination of phosphorus amount and metal element amount in polymer Measured using a fluorescent X-ray analyzer (model number: 3270) manufactured by Rigaku Corporation.
(C) Quantitative determination of the amount of alkali metal in the polymer The quantitative determination was performed by atomic absorption spectrometry (manufactured by Hitachi, Ltd .: polarized Zeeman atomic absorption photometer 180-80, frame: acetylene-air).
(D) Carboxylic acid end-group chip samples and unstretched sheet samples were collected and measured by the method of Maulice et al. (Document MJ Maulice and F. Huizinga, Anal. Chim. Acta, 22 363 (1960)).
(E) Measurement of molecular weight distribution of polymer Molecular weight was measured by GPC method.

Detector: Differential refractive index detector RI
Column: Shodex HFIP-806M
Solvent: Hexafluoroisopropanol Standard: Polyethylene terephthalate (PET-5R, Mw: 55,800) with known molecular weight and quantified polymer of dimethyl terephthalate (F) cyclic trimer are dissolved in hexafluoroisopropanol for high performance liquid chromatography The cyclic trimer was quantified.
(G) Evaluation of hydrolysis resistance (ΔCOOH)
An unstretched film having a thickness of 150 μm was collected and treated in steam at 155 ° C. for 4 hours.
Measuring device: PRESSER COOKER 306SIII (manufactured by HIRAYAMA Corporation)
For ΔCOOH, the amount of carboxylic acid end groups was measured for samples before and after steaming the unstretched film under the above conditions, and the difference between after treatment and before treatment was determined.
(H) Calculation of elongation retention rate Based on ASTM-D882 (1999), the elongation at break of the polyester film was cut into a size of 1 cm × 20 cm and pulled at a chucking distance of 10 cm and a pulling speed of 200 mm / min. The elongation at break was measured. The measurement was performed measurements on 5 samples was breaking elongation E ₀ with its average value. In addition, the elongation retention was obtained by cutting the sample into the shape of a measurement piece (1 cm × 20 cm), treating with a pressure cooker manufactured by Tabai Espec Co., Ltd. for 72 hours under conditions of 125 ° C. and 100% RH. After the time treatment, the breaking elongation of the sample after the treatment was measured based on ASTM-D882 (1999) when it was pulled at a chuck distance of 5 cm and a pulling speed of 200 mm / min. The measurement was performed measurements on 5 samples was breaking elongation E ₁ with its average value. Using the obtained breaking elongations E ₀ and E ₁ , the elongation retention was calculated by the following formula (2).
Elongation retention ratio (%) = E ₁ / E ₀ × 100 (2)
Measurement is performed for the maximum refractive index direction and the minimum refractive index direction of the P layer of the film (when measurement of the refractive index of the P layer is difficult, the measurement is performed for the longitudinal direction (vertical direction) and the width direction (lateral direction)). did.

Measuring device: Film tensile strength measuring device “Tensilon AMF / RTA-100” manufactured by Orientec Co., Ltd.
Sample size: width 10mm x test length 100mm
Tensile speed: 200mm / min
Measurement environment: 23 ° C, 65% RH
An elongation retention of 70% or more, which is considered to correspond to a service life of 30 years or more in solar cell applications, was regarded as acceptable.
(I) OCP Insoluble Quantitative Polymer 1.0 g was dissolved in o-chlorophenol 50 ml at 160 ° C. for 40 minutes and filtered through a glass filter (3G3).
After filtration, the residue was washed with dichloromethane, dried with hot air at 130 ° C. for 10 hours, weighed, and calculated as the ratio of the weight of the residue to the amount of polymer before dissolution (wt%).
(J) Measurement of pH Phosphoric acid and alkali metal phosphate were weighed to a total of 2 g, dissolved in 100 ml of ethylene glycol, and then pH was measured.
Measuring device: AT-510 (manufactured by Kyoto Electronics Industry Co., Ltd.)
(K) Plane orientation coefficient fn
Using a sodium D line (wavelength 589 nm) as a light source, the refractive index in the plane direction and the refractive index in the thickness direction of the film are measured using an Abbe refractometer. The sample is then rotated every 10 ° and a similar measurement is performed 360 °. From the in-plane distribution of the obtained refractive index, Nmax is the refractive index of the maximum refractive index, Nmin is the refractive index in the in-plane 90 ° direction from that direction, and Nz is the average value of the refractive indexes in the respective thickness directions. The plane orientation coefficient (fn) was calculated from (3).
Plane orientation coefficient fn = (Nmax + Nmin) / 2-Nz (3)
Example 1
A transesterification reactor was charged with 100 parts by weight of dimethyl terephthalate, 0.65 parts by weight of trimethyl trimellitic acid, 57.5 parts by weight of ethylene glycol, 0.06 parts by weight of magnesium acetate tetrahydrate, and 0.03 parts by weight of antimony trioxide. After melting at the bottom, the temperature was raised to 230 ° C. over 3 hours with stirring, and methanol was distilled off to conduct a transesterification reaction.

After the transesterification reaction, an ethylene glycol solution in which 0.019 part by weight of phosphoric acid (equivalent to 1.9 mol / ton) and 0.027 part by weight of sodium dihydrogen phosphate dihydrate (equivalent to 1.7 mol / ton) were dissolved in 0.5 part by weight of ethylene glycol (PH 5.0) was added.

The reaction product was transferred to a polymerization apparatus, the pressure was reduced while raising the temperature from 230 ° C. to 280 ° C., and the polycondensation reaction was performed at a final temperature of 280 ° C. and a vacuum of 0.1 Torr. In this way, polyethylene terephthalate having an intrinsic viscosity of 0.54 and a COOH end group of 11 equivalents / ton was obtained.

The obtained polyethylene terephthalate was dried and crystallized at 160 ° C. for 6 hours, and then subjected to solid phase polymerization for 8 hours under the conditions of 220 ° C. and a vacuum degree of 0.3 Torr, and an intrinsic viscosity of 0.85, COOH end groups of 8.0 equivalent / ton, Polyethylene terephthalate having a cyclic trimer content of 0.27 wt% was obtained. The copolymerization amount of the trimellitic acid component of this polyethylene terephthalate was 0.50 mol%, Mw / Mn was 6.5, the number average molecular weight was 11,200, and the melting point Tm was 255 ° C. As described above, the alkaline earth metal species was magnesium, the amount was 2.8 mol / ton, the amount of phosphorus element was 3.6 mol / ton, and the molar ratio of alkaline earth metal / phosphorus element was 0.77. Moreover, OCP insoluble matter was 0.0 wt%.

Polyethylene terephthalate after solid phase polymerization was supplied to an extruder in a nitrogen atmosphere, quenched at a casting drum (20 ° C.) from a T die at an extrusion temperature of 280 ° C., and converted into a sheet by an electrostatic application method to obtain an unstretched film. Later, the film was longitudinally stretched at a longitudinal stretching temperature of 90 ° C. and a longitudinal stretching ratio of 3.8 times, and then stretched at a transverse stretching temperature of 110 ° C. and a transverse stretching ratio of 3.8 times. As a result, a biaxially stretched film was obtained. Tm-Th was 45 ° C.

At this time, a 400-mesh wire mesh was used for the filter of the extruder, and the residence time was about 3 minutes from the supply of the polymer to the discharge from the T-die.

When the hydrolysis resistance was evaluated, the COOH end group of the unstretched film before treatment was 10 equivalent / ton, and the COOH end group after treatment under steam at 155 ° C. for 4 hours was 33 equivalent / ton. Therefore, ΔCOOH Was 23 eq / ton.

Furthermore, the obtained biaxially stretched film was compared for film elongation before and after treatment at 125 ° C., 100% RH, 72 hours, and the elongation retention was calculated. There was no problem level.
(Example 2)
A slurry consisting of 86 parts by weight of terephthalic acid and 37 parts by weight of ethylene glycol was supplied to an esterification reactor pre-charged with 114 parts by weight of bishydroxyethylene terephthalate (equivalent to 100 parts by weight of PET) by a snake pump over 3 hours. The esterification reaction was carried out while controlling the temperature of the product at 245 ° C to 255 ° C.
After completion of the esterification reaction, 114 parts by weight of the obtained bishydroxyethylene terephthalate (equivalent to 100 parts by weight of PET) was transferred to a polymerization can, 0.06 parts by weight of magnesium acetate tetrahydrate, 0.03 parts by weight of antimony trioxide, trimellitic anhydride A slurry of 0.50 part by weight / 16.1 parts by weight of ethylene glycol (0.5 mole times the total acid component) was sequentially added, and the reaction was continued for 30 minutes with stirring to distill water. Thereafter, an ethylene glycol solution (pH 5.0) containing 0.019 part by weight of phosphoric acid (equivalent to 1.9 mol / ton) and 0.027 part by weight of sodium dihydrogen phosphate dihydrate (equivalent to 1.7 mol / ton) in 0.5 part by weight of ethylene glycol. ), The pressure is reduced while raising the temperature from 255 ° C. to 280 ° C., and the polycondensation reaction is carried out at a final ultimate temperature of 280 ° C. and a vacuum degree of 0.1 Torr. The polyethylene has an intrinsic viscosity of 0.54 and COOH end groups of 12 equivalents / ton. Terephthalate was obtained.

The obtained polyethylene terephthalate was dried and crystallized at 160 ° C. for 6 hours, and then subjected to solid phase polymerization for 8 hours under the conditions of 220 ° C. and a vacuum degree of 0.3 Torr, and an intrinsic viscosity of 0.85, COOH end groups of 8.0 equivalent / ton, Polyethylene terephthalate having a cyclic trimer content of 0.29 wt% was obtained. The copolymerization amount of the trimellitic acid component of this polyethylene terephthalate was 0.50 mol%, Mw / Mn was 6.5, the number average molecular weight was 11,500, and the melting point Tm was 255 ° C. As described above, the alkaline earth metal species was magnesium, the amount was 2.8 mol / ton, the amount of phosphorus element was 3.6 mol / ton, and the molar ratio of alkaline earth metal / phosphorus element was 0.77. Moreover, OCP insoluble matter was 0.0 wt%.
Further, a biaxially stretched film was obtained through an unstretched film under the same conditions as in Example 1 and an effective surface ratio of 13.2 times under the same stretching conditions as in Example 1. Tm-Th was 45 ° C. When the hydrolysis resistance was evaluated, the COOH end group of the unstretched film before treatment was 10 equivalent / ton, and the COOH end group after treatment under steam at 155 ° C. for 4 hours was 33 equivalent / ton. Therefore, ΔCOOH Was 23 eq / ton.

Furthermore, the obtained biaxially stretched film was compared for film elongation before and after treatment at 125 ° C., 100% RH, 72 hours, and the elongation retention was calculated. There was no problem level.
(Examples 3-9, 11, 12, Comparative Examples 1-3)
The polyethylene terephthalate composition having a melting point Tm of 255 ° C., except that the types and addition amounts of various additives are changed as shown in Tables 2 to 4 and the draw ratio is changed to the following conditions. And the biaxially stretched film was obtained.
In Example 3, after longitudinal stretching at a longitudinal stretching temperature of 90 ° C. and a longitudinal stretching ratio of 3.8 times, stretching was performed at a transverse stretching temperature of 110 ° C. and a transverse stretching ratio of 3.8 times, and the heat treatment temperature Th was 210 ° C. for 3 seconds. The surface magnification was 10.2. In Example 4, after longitudinal stretching at a longitudinal stretching temperature of 90 ° C. and a longitudinal stretching ratio of 3.5 times, stretching was performed at a transverse stretching temperature of 110 ° C. and a transverse stretching ratio of 3.5 times, and the heat treatment temperature Th was 210 ° C. for 3 seconds. The surface magnification was 12.1 times. In Example 5, after longitudinal stretching at a longitudinal stretching temperature of 90 ° C. and a longitudinal stretching ratio of 3.3 times, stretching was performed at a transverse stretching temperature of 110 ° C. and a transverse stretching ratio of 3.3 times, and the heat treatment temperature Th was 210 ° C. for 3 seconds. The surface magnification was 9.5 times. In Example 6 to Example 9, Example 11, Example 12, and Comparative Example 1 to Comparative Example 3, as in Example 1, after longitudinal stretching at a longitudinal stretching temperature of 90 ° C. and a longitudinal stretching ratio of 3.8 times, Stretching was performed at a stretching temperature of 110 ° C. and a transverse stretching ratio of 3.8 times, and the heat treatment temperature Th was set at 210 ° C. for 3 seconds to obtain an effective surface ratio of 13.2 times. In these examples and comparative examples, Tm-Th was 45 ° C.
In Example 3, the content of the trifunctional or higher functional copolymer component is 0.03 mol%, which is close to the lower limit, Mw / Mn is 5.3 as small as Example 1, and the effective surface magnification is low as 10.2 times. , 125 ° C., 100% RH, elongation retention after 72 hours of treatment tended to be slightly reduced to 75%, but it was at a level that would not cause any problems even when used for solar cell applications.

In Example 4, since the content of the tri- or higher functional copolymer component is close to the upper limit of 0.90 mol%, Mw / Mn tends to increase to 7.7, and OCP insoluble matter tends to increase to 0.30 wt%. However, since the number average molecular weight is lower than 9,300 and 10,000, the elongation retention after treatment at 125 ° C, 100% RH and 72 hours tends to decrease slightly to 73%. There was no level.

In Example 5, since the effective surface magnification is less than 9.5 times and 10 times, the elongation retention after treatment at 125 ° C., 100% RH and 72 hours tends to decrease to 73%. It was at a level where there was no problem even if it was used.

In Example 6, since no alkaline earth metal compound was added, the electrostatic application characteristics were slightly insufficient, and the thickness unevenness of the film tended to increase slightly. In addition, since the content of alkali metal is 1.2 mol / ton, that is, the content of sodium dihydrogen phosphate is close to the lower limit, ΔCOOH tends to be a little as high as 35 equivalents / ton. There was no problem level.

In Examples 7 and 8, the reaction was carried out by polycondensation reaction to an intrinsic viscosity of 0.65, and the solid phase polymerization time was shortened accordingly, so that the amount of COOH end groups of the polymer increased slightly to 13 eq / ton and 14 eq / ton, respectively. However, even if it was used for solar cell applications, it was at a level where there was no problem.

In Example 9, since the phosphorus element content was close to the upper limit of 4.8 mol / ton and the pH of the ethylene glycol solution of phosphoric acid and sodium dihydrogen phosphate was 3.0, the acidity was strong, so ΔCOOH was 43 Equivalent / ton is somewhat large, but it was at a level that would not cause any problems even when used for solar cell applications.

In Comparative Example 1, since it does not contain a tri- or higher functional copolymer component, Mw / Mn is insufficient as 3.4, and the elongation retention after treatment at 125 ° C., 100% RH and 72 hours is 53%. It was not a satisfactory level.

In Example 11, the amount of phosphorus element is 1.8 mol / ton, the amount of alkali metal is 1.0 mol / ton, and the amount of magnesium metal is 1.7 mol / ton, which is smaller than that of Example 1. In Example 12, the amount of phosphorus element is Is slightly higher at 3.0 mol / ton, alkali amount is 1.0 mol / ton, and magnesium metal content is as low as 1.9 mol / ton, so ΔCOOH tends to be slightly higher at 30 equivalents / ton and 27 equivalents / ton, respectively. It was at a level that would not cause any problems.

In Comparative Example 2, the amount of phosphorus element is 1.1 mol / ton and the amount of alkali metal is 0.0 mol / ton, both of which are outside the range defined in the present invention, so that a sufficient hydrolysis reaction inhibiting effect cannot be obtained, The elongation retention after treatment at 125 ° C. and 100% RH for 72 hours was unsatisfactory at 33%.

In Comparative Example 3, since 1.2 mol% of the trifunctional or higher functional crosslinking component exceeds the upper limit of the range specified in the present invention, a large amount of OCP insoluble matter of 68 wt% is generated and can be processed into a film. No polyethylene terephthalate composition could be obtained.
(Example 10)
A polyethylene terephthalate composition having a melting point Tm of 255 ° C. was obtained in the same manner as in Example 2 except that trimellitic anhydride was added in the form of a slurry in an amount of 4.0 parts by weight of ethylene glycol (corresponding to 0.13 moles relative to the total acid component). After that, the film was made into an unstretched film, and the stretching conditions were the same as in Example 2. The film was stretched at a longitudinal stretching temperature of 90 ° C. and a longitudinal stretching ratio of 3.8 times, and then stretched at a transverse stretching temperature of 110 ° C. and a transverse stretching ratio of 3.8 times. Th was set at 210 ° C. for 3 seconds to obtain a biaxially stretched film having an effective surface magnification of 13.2 times. Tm-Th was 45 ° C.

Since the amount of ethylene glycol added after the esterification reaction was less than that in Example 2, the amount of COOH end groups of the polymer tended to increase to 16 equivalents / ton, but this was problematic even when used for solar cell applications. There was no level.
(Example 13)
100 parts by weight of dimethyl terephthalate, 57.5 parts by weight of ethylene glycol, 0.07 parts by weight of manganese acetate tetrahydrate and 0.03 parts by weight of antimony trioxide were charged into a transesterification reactor, melted at 150 ° C. in a nitrogen atmosphere, and then stirred. The temperature was raised to 230 ° C. over 3 hours, methanol was distilled off, and a transesterification reaction was performed.

After completion of the transesterification reaction, 0.1 part by weight of trimellitic anhydride was added as a 10 wt% ethylene glycol solution. After stirring for 10 minutes, 0.019 part by weight of phosphoric acid (equivalent to 1.9 mol / ton) and sodium dihydrogen phosphate dihydrate were added. An ethylene glycol solution (pH 5.0) in which 0.027 parts by weight (equivalent to 1.7 mol / ton) was dissolved in 0.5 parts by weight of ethylene glycol was added.

The reaction product was transferred to a polymerization apparatus, the pressure was reduced while raising the temperature from 230 ° C. to 280 ° C., and the polycondensation reaction was performed at a final temperature of 280 ° C. and a vacuum of 0.1 Torr. In this way, polyethylene terephthalate having an intrinsic viscosity of 0.58 and a COOH end group of 12 equivalents / ton was obtained.

The obtained polyethylene terephthalate was dried and crystallized at 160 ° C. for 6 hours, and then subjected to solid phase polymerization for 8 hours under the conditions of 228 ° C. and a vacuum degree of 0.3 Torr, and an intrinsic viscosity of 0.81, COOH end groups of 8.0 equivalent / ton, Polyethylene terephthalate having a cyclic trimer content of 0.28 wt% was obtained. The polyethylene terephthalate had a Mw / Mn of 6.0, a number average molecular weight of 10,800, and a melting point Tm of 255 ° C. The alkaline earth metal species was manganese as described above, and the amount thereof was 2.8 mol / ton, the amount of phosphorus element was 3.6 mol / ton, and the OCP insoluble matter was 0.0 wt%.
Furthermore, a biaxially stretched film was obtained under the same stretching conditions as in Example 1 through an unstretched film under the same conditions as in Example 1. Tm-Th was 45 ° C. Since manganese is used in place of the alkaline earth metal, the electrostatic application characteristics tend to be slightly lower than in Example 1 and the thickness unevenness tends to be slightly larger. Tended to be good. This is presumably because manganese, which is a transition metal, is not as much as alkaline earth metal, but contributes to improvement of electrostatic application characteristics. As shown in Table 5, the physical properties of the obtained biaxially stretched film were almost the same as those of Example 1, and were at a level that would not cause any problems even when used for solar cell applications.
(Examples 14 to 24)
A polyethylene terephthalate composition having a melting point Tm of 255 ° C. was obtained in the same manner as in Example 13 except that the addition amount of various copolymerization components was changed, and an unstretched film was obtained. Using the obtained unstretched film, a biaxially stretched film was obtained in the same manner as in Example 1 except that the stretching conditions were as follows.
In Example 14, after longitudinal stretching at a longitudinal stretching temperature of 90 ° C. and a longitudinal stretching ratio of 3.8 times, stretching was performed at a transverse stretching temperature of 110 ° C. and a transverse stretching ratio of 3.8 times, and the heat treatment temperature Th was 220 ° C. for 3 seconds. The surface magnification was 13.2 times (Tm−Th is 35 ° C.). In Example 15, after longitudinal stretching at a longitudinal stretching temperature of 90 ° C. and a longitudinal stretching ratio of 3.8 times, stretching was performed at a transverse stretching temperature of 110 ° C. and a transverse stretching ratio of 3.8 times, and the heat treatment temperature Th was 200 ° C. for 3 seconds. The surface magnification was 13.2 times (Tm-Th is 55 ° C.). In Example 16, after longitudinal stretching at a longitudinal stretching temperature of 87 ° C. and a longitudinal stretching ratio of 3.8 times, stretching was performed at a transverse stretching temperature of 100 ° C. and a transverse stretching ratio of 3.8 times, and the heat treatment temperature Th was 200 ° C. for 3 seconds. The surface magnification was 13.2 times (Tm-Th is 55 ° C.). In Example 17, after longitudinal stretching at a longitudinal stretching temperature of 87 ° C. and a longitudinal stretching ratio of 3.8 times, stretching was performed at a transverse stretching temperature of 100 ° C. and a transverse stretching ratio of 4.2 times, and the heat treatment temperature Th was 200 ° C. for 3 seconds. The surface magnification was 14.6 times (Tm-Th is 55 ° C.). In Examples 18 to 20, the film was stretched longitudinally at a longitudinal stretching temperature of 87 ° C. and a longitudinal stretching ratio of 3.8 times, and then stretched at a transverse stretching temperature of 100 ° C. and a transverse stretching ratio of 4.5 times. Second, the effective surface magnification was 15.6 times (Tm-Th is 55 ° C.). In Examples 21 to 23, the film was stretched at a longitudinal stretching temperature of 90 ° C. and a longitudinal stretching ratio of 3.8 times, and then stretched at a transverse stretching temperature of 100 ° C. and a transverse stretching ratio of 4.5 times. Second, the effective surface magnification was 15.6 times (Tm-Th is 55 ° C.). In Example 24, after longitudinal stretching at a longitudinal stretching temperature of 90 ° C. and a longitudinal stretching ratio of 3.8 times, stretching was performed at a transverse stretching temperature of 100 ° C. and a transverse stretching ratio of 3.8 times, and the heat treatment temperature Th was 200 ° C. for 3 seconds. The surface magnification was 13.2 times (Tm-Th is 55 ° C.).

  In Example 14, since the heat treatment temperature Th was set to 220 ° C. which was 10 ° C. higher than that in Example 13, the elongation retention after treatment for 125 ° C., 100% RH and 72 hours tends to decrease to 77%. However, even if it was used for solar cells, it was at a level where there was no problem. It is estimated that since the heat treatment temperature Th was increased, the amorphous portion was relaxed and embrittlement was slightly advanced in the wet heat treatment.

In Example 15, since the heat treatment temperature Th was set to 200 ° C., which was 10 ° C. lower than that in Example 13, the elongation retention after treatment for 125 ° C., 100% RH and 72 hours was 87%, 125 ° C., 100 % RH, the elongation retention after 96 hours treatment tended to improve to 5.0%, which was a sufficient level for solar cell applications. On the other hand, since the heat treatment temperature Th was made lower than that of Example 13, the average of the heat shrinkage rate in the vertical and horizontal directions when heat-treated at 150 ° C. for 30 minutes was 2% to 3%. And the heat shrinkage rate tended to be slightly larger.
In Example 16, since the longitudinal stretching temperature (87 ° C.), the transverse stretching temperature (100 ° C.), and the heat treatment temperature Th (200 ° C.) were set lower than in Example 13, 125 ° C., 100% RH, 72 The elongation retention after the time treatment was 88%, 125 ° C., 100% RH, and the elongation retention after 96 hours treatment tended to improve to 7.0%, which was a sufficient level for solar cell applications. Furthermore, since the stretching temperature is low as compared with Example 15, the plane orientation coefficient fn increased to 0.165, the elongation retention after treatment at 125 ° C., 100% RH, 72 hours, and the elongation after 96 hours treatment. There was a tendency for the degree of retention to improve.
In Examples 17 and 18, since transverse stretching was performed at a higher magnification (lateral stretching magnifications 4.2 times, 4.5 times) than Example 16 (lateral stretching magnification 3.8 times), the plane orientation coefficient fn was proportional to the stretching magnification. Increased to 0.168 and 0.171, and the elongation retention after treatment at 125 ° C, 100% RH and 72 hours (88%, 89%) and the elongation retention after 96 hours (15%, 23%) are improved. It was in a tendency and was a sufficient level for solar cell applications.
In Example 19, except that the polymer was supplied to the extruder under a dehumidified air atmosphere, film formation and evaluation were performed under the same conditions as in Example 18, so that the intrinsic viscosity IV of the unstretched film was reduced to 0.71, and unstretched The COOH end groups of the film increased to 13 mol / ton, and both the elongation retention (87%) after treatment for 72 hours and 125 ° C, 100% RH and the elongation retention (8.0%) after treatment for 96 hours decreased. Although there was a tendency, it was a sufficient level for solar cell applications. Compared to Example 18, it is presumed that the intrinsic viscosity IV of the film decreased and the COOH end groups of the film increased due to accelerated oxidative degradation by oxygen in the dehumidified air.
In Example 20, when the film formation was evaluated under the same conditions as in Example 19 except that the polymer filter was reinforced and the residence time was 20 minutes, the intrinsic viscosity IV of the unstretched film was higher than that in Example 19. Reduced to 0.68, COOH end groups of unstretched film increased to 16 mol / ton, elongation retention (85%) after treatment at 125 ° C, 100% RH, 72 hours, and elongation retention after treatment for 96 hours Both (3.0%) tended to decrease slightly, but at a level that was not a problem for solar cell applications. Compared to Example 18, it is presumed that the thermal viscosity was accelerated due to the longer residence time, so that the intrinsic viscosity IV of the film decreased and the COOH end groups of the film increased.
In Example 21, the amount of trimellitic anhydride copolymerization was changed to 0.07 mol%, the transverse draw ratio was 4.5 times higher than in Example 13, and the transverse draw temperature and heat treatment temperature Th were 10 ° C. compared to Example 13. Since it was set to 200 ° C., the plane orientation coefficient fn increased to 0.171 compared to Example 13, and the elongation retention (88%) after treatment at 125 ° C. and 100% RH for 72 hours and after 96 hours treatment. There was a tendency for the elongation retention rate (22%) to improve, which was a sufficient level for solar cell applications. Moreover, although the stretching temperature is higher than that of Example 18, it is presumed that the equivalent plane orientation coefficient was obtained because the amount of trimellitic anhydride copolymer was small and the orientation was easy.
In Example 22, the trimellitic anhydride copolymerization amount was changed to 0.20 mol%, the transverse draw ratio was 4.5 times higher than Example 13, and the heat treatment temperature Th was 10 ° C. lower than Example 13 and 200 ° C. Since it was set, the plane orientation coefficient fn was increased to 0.170 compared with Example 13, and the elongation retention (87%) after treatment at 125 ° C. and 100% RH for 72 hours and the elongation retention after 96 hours treatment. The rate (20%) tended to improve, which was a sufficient level for solar cell applications. In addition, it is estimated that the reason why the plane orientation coefficient is lower than that in Example 21 is that the trimellitic anhydride copolymerization amount is large, so that the orientation becomes difficult.
In Example 23, the amount of trimellitic anhydride copolymerization was changed to 0.05 mol%, the transverse draw ratio was 4.5 times higher than in Example 13, and the transverse draw temperature and heat treatment temperature Th were 10 ° C. compared with Example 13. Since the temperature was set to 200 ° C., the plane orientation coefficient fn increased to 0.171, and the elongation retention (87%) after treatment at 125 ° C., 100% RH and 72 hours and elongation retention (10% after treatment for 96 hours) %) Tended to improve, and the level was sufficient for solar cell applications. On the other hand, when compared with Examples 21 and 22, the elongation retention after treatment at 125 ° C. and 100% RH for 72 hours and the elongation after treatment for 96 hours despite having an equivalent plane orientation coefficient. It is presumed that the retention rate tends to decrease slightly due to the amount of trimellitic anhydride copolymerized.
In Example 24, the amount of trimellitic anhydride copolymerization was changed to 0.50 mol%, the transverse draw ratio was 3.8 times, the same conditions as in Example 13, and the transverse draw temperature and heat treatment temperature Th were 10 as compared with Example 13. Since the temperature was set to 200 ° C. lower, the plane orientation coefficient fn increased to 0.168, and the elongation retention (87%) after treatment at 125 ° C., 100% RH and 72 hours tends to be improved as compared with Example 13. Yes, it was a sufficient level for solar cell applications. On the other hand, as compared with Examples 21 and 22, the plane orientation coefficient fn slightly decreased to 0.168 as described above, and the elongation retention (87%) after treatment at 125 ° C. and 100% RH for 72 hours and after 96 hours treatment. It is presumed that the elongation retention rate (1.0%) tends to decrease slightly due to the copolymerization amount of trimellitic anhydride.
In any of the examples, it was at a level where there was no problem even if it was used for solar cell applications, but the elongation retention rate was higher in Examples 15 to 21 and further higher in Examples 18, 21, and 22. I understood it.
(Example 25)
Polyethylene terephthalate having an intrinsic viscosity of 0.58 and a COOH end group of 14 equivalents / ton was obtained in the same manner as in Example 11 except that sodium dihydrogen phosphate dihydrate and trimellitic anhydride were not added.

The obtained polyethylene terephthalate was dried and crystallized at 160 ° C. for 6 hours, and then subjected to solid phase polymerization for 8 hours under the conditions of 228 ° C. and a vacuum degree of 0.3 Torr, and an intrinsic viscosity of 0.82, COOH end groups of 10 equivalents / ton, Polyethylene terephthalate for lamination having a cyclic trimer content of 0.28 wt% was obtained. The polyethylene terephthalate had a Mw / Mn of 3.2, a number average molecular weight of 10,800, and a melting point Tm of 255 ° C.
The obtained polyethylene terephthalate for lamination was vacuum dried at a temperature of 180 ° C. for 3 hours and then supplied to the sub-extruder. In addition to the sub-extruder, a main extruder was used, and this main extruder was polymerized in the same manner as in Example 13 and had an intrinsic viscosity of 0.80 and a carboxyl group terminal number of 8.0 equivalents / ton (glass transition temperature). 83 ° C., melting point 255 ° C.) was vacuum dried for 3 hours and then fed to the main extruder. Each of the component layers fed to the sub-extruder is melted at a temperature of 280 ° C. in a nitrogen atmosphere, and then supplied to the sub-extruder on both sides of the component layer supplied to the main extruder. Component layer: Component layer of sub-extruder = 1: 6: 1 Combined, melted three-layer lamination co-extrusion from T die die, laminated sheet, drum maintained at a surface temperature of 20 ° C. The film was cooled and solidified by close contact with an electrostatic application method to obtain an unoriented (unstretched) laminated film. The obtained laminated sheet was biaxially stretched and heat-treated under the same conditions as in Example 1 to obtain a laminated biaxially stretched film. Tm-Th was 45 ° C. Table 8 shows the results of evaluating the properties of the obtained film. As shown in Table 8, each physical property of the obtained biaxially stretched film is formed by laminating layers not containing a crosslinking component, so that the elongation retention after treatment at 125 ° C., 100% RH, 72 hours is 75. %, Which is slightly lower than that of Example 1 (86%), but it was at a level that does not pose a problem even when used for solar cell applications.
(Comparative Example 4)
Except for changing the copolymerization amount of trimellitic anhydride to 0.05 mol%, changing the melt polymerization temperature to 290 ° C, discharging at an intrinsic viscosity of IV 0.65, and setting the intrinsic viscosity IV after solid weight to 0.70 and Mw / Mn to 4.5 A biaxially stretched film was obtained through the unstretched film in the same manner as in Example 10 under the same stretching conditions as in Example 10. Tm-Th was 45 ° C. As shown in Table 4, the physical properties of the obtained biaxially stretched film are outside the range defined by the present invention, so that the elongation retention after treatment at 125 ° C., 100% RH and 72 hours is 40%. % Was insufficient for solar cell applications.
(Example 26)
A biaxially stretched film was obtained in the same manner as in Example 18 except that 0.07 part by weight of manganese acetate tetrahydrate was changed to 0.5 part by weight of calcium acetate tetrahydrate. Tm-Th was 55 ° C. Table 9 shows the results of evaluating the properties of the obtained film. Compared to Example 18, the OCP insoluble matter tended to increase to 0.10 wt%, but it was at a level that would not cause any problems even when used for solar cells. It is presumed that the cause of the increase in OCP insoluble matter was that calcium acetate reacted during the polymerization reaction to form internally precipitated particles such as calcium terephthalate.

The composition of the present invention is made into a biaxially stretched film, so that it is necessary for applications such as magnetic materials, electrical materials such as capacitors, and packaging applications, in particular, long-term hydrolysis resistance and elongation retention. It can provide for the film use for solar cells.

1: Back sheet 2: Filler 3: Power generation element 4: Transparent substrate 5: Sunlight

Claims (14)

A polyethylene terephthalate composition containing from 0.01 mol% to 1.00 mol% of a tri- or higher functional copolymer component with respect to the ethylene terephthalate unit, and the ratio of the weight average molecular weight to the number average molecular weight (Mw / Mn) is from 5.0 to 8.0. The alkali metal compound is 1.0 mol / ton to 3.0 mol / ton as an alkali metal element, the phosphorus compound is 1.5 mol / ton to 5.0 mol / ton as a phosphorus element, and o-chlorophenol insoluble matter is 0.50. Polyethylene terephthalate composition that is less than wt%. The polyethylene terephthalate composition according to claim 1, wherein the COOH end group content is 15 equivalents / ton or less, and the cyclic trimer content is 0.50 wt% or less. 3. The polyethylene terephthalate composition according to claim 1, wherein a COOH end group increase (ΔCOOH) when treated at 155 ° C. for 4 hours under steam is 40 equivalents / ton or less. The polyethylene terephthalate composition according to any one of claims 1 to 3, wherein a molar ratio of the alkaline earth metal element and the phosphorus element is 0.5 or more and 1.5 or less. The polyethylene terephthalate composition according to any one of claims 1 to 4, wherein the phosphorus compound is phosphoric acid or an alkali metal phosphate. Phosphoric acid and alkali phosphate adjusted to pH 2.0 or more and 6.0 or less when producing a polyethylene terephthalate composition through esterification reaction or transesterification reaction using terephthalic acid component, ethylene glycol, trifunctional or higher copolymerization component A method for producing a polyethylene terephthalate composition, wherein an ethylene glycol solution or slurry of a metal salt is added until the esterification reaction or transesterification reaction is substantially completed and the polycondensation reaction is started. When producing a polyethylene terephthalate composition through an esterification reaction using terephthalic acid, ethylene glycol, and a tri- or higher functional copolymer component, 0.3 to 0.5 times mole of ethylene with respect to the total acid component The method for producing a polyethylene terephthalate composition according to claim 6, wherein the glycol is added during a period until the esterification reaction is substantially completed and the polycondensation reaction is started. A polyethylene terephthalate film comprising at least one polyethylene terephthalate film layer comprising the polyethylene terephthalate composition according to claim 1. The polyethylene terephthalate film according to claim 8, wherein the polyethylene terephthalate film layer has a plane orientation coefficient of 0.150 or more. The polyethylene terephthalate film according to any one of claims 8 to 9, wherein the polyethylene terephthalate film layer has a COOH end group amount of 20 equivalent / ton or less. The polyethylene terephthalate film according to any one of claims 8 to 10, wherein the intrinsic viscosity (IV) of the polyethylene terephthalate film layer is 0.65 or more. The polyethylene terephthalate film according to claim 8, wherein the elongation retention after treatment at 125 ° C, 100% RH and 72 hours is 70% or more. A method for producing a polyethylene terephthalate film according to claim 8, wherein the polyethylene terephthalate film is subjected to heat treatment in a temperature range satisfying the following formula (1) after biaxially stretching the unstretched film.
35 ° C ≦ Tm−Th ≦ 90 ° C (1)
Here, Tm: melting point of polyethylene terephthalate composition (° C.), Th: heat treatment temperature (° C.) A solar battery back sheet comprising the polyethylene terephthalate film according to claim 8.

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